Pressure increase in room connected to cannister

I have a Helium cannister at 500bar pressure with a flow restrictor supplying Helium at 8 bar pressure to a room of 24m^3 at 1 bar pressure. The Helium flows down a 50m pipe. I want to calculate the pressure increase in the room due to the Helium in the event that the flow restrictor fails and the entire 500bar pressure is exerted on the pipe.

I have used the Hagen-Poiseuille equation to get an expression for the volume flow rate and the pressure drop, however I have not performed these kinds of calculations before and so I am unsure if I am going down the correct path.

My initial thoughts were to take the normal pressure drop between the cannister and the room as 7 bar, then calculate the volume flow rate due to this pressure drop. In a given time of an hour, the pressure in the room should increase from Pair to Pair + Phelium. The pressure of the helium can be calculated using the ideal gas law equation PV=nRT. The process can then be repeated with the higher pressure of 500 bar.

This route seems riddled with holes to me. Is there a more simple/accurate approach to the problem?

The next issue is that I want to add a flow restrictor to reduce the pressure in the pipe. The room can evacuate 50m3/hr of gas, which equates to 0.014 m3/s. I want to restrict the flow entering the room to this level to prevent the pressure increasing.

I thought that the Hagen-Poiseuille equation would work, but it appears to be only useful for laminar flow. The Reynold's number for this setup puts it firmly in the turbulent category, so should I use the Darcy-Weisbach equation?

For your flow restriction, were you going to use an orifice, a valve, or just striaght pipe? Both compressibility and viscous effect will be important.

With your pressure differences, your flow will likely be choked (limited by the speed of sound). For any component, if the downstream pressure drops below about 50% of the inlet pressure, the flow will be choked.